Electrothermic reduction of iron ores



Dec. 22, 1931. s. T. wlLEs ELECTROTHERMIC REDUCTION OF IRON ORES 2 sheets-smet 2 Filed Dec. 7, '1928 Patented Dec. 22, 1931 lSYDNEY W'ILES, OF BUFFALO, NEW' YORK, lASSIGNOR TO CORPORATION, OF BUFFALO,

ELECTROTHRMIC REDUCTION OF IRON Application led December 7, 1928. Serial No. 324,505. possibly 3000 FL at the base to400 or This invention relates to a method of and apparatus for 4the electrothermic reduction of iron ores or similar compounds, and it particularly relates to a method 'of reduction wherein the ore is finely divided and j h'omogeneously admixed with a reducing a ent such as charcoal and a fluxing agent suc as lime, and the mixture introduced into a closed tube leading directly into an electric arc, the finel divided materials being4 protected from blasts of waste gases until reduced to such condition as to be substantially metalliferous in character when the materials are elevated to a temperature insuring complete reduction, and to apparatus for utilizing this and similar processes.

The extraction of iron from its ores is one l of the oldest of known metallurgical procl esses. Of the various methods that have been proposed, two in particular have survived and are now in use. One method, the blast furnace method, which is universally ernployed, consists in feedin crushed iron ore, such as hematite. Fega, or magnetite, Fe3O4, (the naturally occurring oxides of iron) or ores converted into oxide form by roasting, such as the carbonate or sulfide, into the top of a blast furnace. This apparatus consists of a tall stack provided with means at its lower portion for the introduction of a blast of hot air. Disposed in alternating layers with the ore are layers or strata of carbon in the form of coke and a liuxing material such as lime. The reactions' of the reduction process are many and complex,but,in its essence, the action consists inburning the lower layers of coke with the hot air, to form carbon monoxide and carbon dioxide,-hot gases which flow upwardly through the charge to effect the extraction of oxygen from the iron oxide, producing ultimately a layer of impure and molten iron (pig iron) at the bottom of the furnace, on which floats a liquid layer of slag consisting of the gangue of the ore, the fluxing agent, and various impurities of the. ore which preferentially react with the lime.

As stated, there are many individual reactions occurring in the furnace, depending primarily on the temperature which varies Nr OFFICE NEW YORK, A. CORPORATION from 500 F. at the point of exit of waste gases.

At lcertain temperatures carbonreacts-di-v forming metallic .iron and carbon dioxide,-

4rectly with iron oxide, and carbon monoxide while at other temperatures therel are formed by 'the same ingredients another forml of oxide of iron, FeO, and carbon monoxide. The gases liberated in one portion of the stack move upwardly, reacting bothv with carbon and ore, depending upon the' specific wILEs nnnofrarc mannen EISSU-ED conditions-iebtaining. The blast furnace method has-4 been so extensively used and studied that detailed explanation would notbe in order here, suilice it to understand, from the foregoing comment', that the reducing action is rimarily effected by the reaction of hot car on monoxide on the raw ore.

During the past quarter century considerable serious study has been given to the electrothermic reduction of iron ore,-reduction of-oreto metal by the heat of' an electric arc o'r by means of a current of electricity flowing through the coils of a transformer. Except for certain localities 4where economic conditions are favorable, have notsupplanted the blast furnace process. A more extensive use has been found for such reduction processes wherein the` roduct soughtwas an iron alloy, such aserron' silicon, ferro-nickel, or the like,but the basic principles of the reducing action for these these processes nsy as those employed in the electrothermic manufacture of pig iron. Accordingly, the latter manufacture may be referred to for examples sake. I

c Of the various proposals for the utilization of the electric arc in ore reduction, three may be noted here.` The most satisfactory proc.- ess involves the reduction of the ore in a. stack furnace, the'ore, carbon, and iux being fed into a tower, reacting with a circulating blast of reducing gases, and finally being treated in an arc furnace disposed at the bottom of the tower. Like the blast furnace method, this process depends .upon reduction by gases generated by the action .of -a blast of hot air on the carbon in the charge.

' Another',and even more direct gaseous method .of reduction, has been attempted in the ftreatment in separate apparatus.

laboratory by passing a current of carbon monoxide at an appropriate velocity and temperature over a batch of ore (and .linx- .ing agent) contained in a quartz tube. Es-

separate apparatus may be, (according to `the reports of this method)y similar to ythat lemployed'in an electrothermic method in `which apot serving as a furnace, is filled with crushed fore, carbon, and flux, and sub- 'ected to the action of an electric are playing. through the mixture. Fresh vquantities of chargema be added'through a chute disposed lover t e furnace, entering .in a cold condition. Waste furnace gases are not ydi- .passing them through the lincoming char e, being diverted from the -furnace throng a separate pipe. In this method, the reducing action 1s more essentially directly betweenelemental carbon and ore. As stated,`the charge for this furnace may consistof the vpartially kreduced material obtained by .gas reduction, 'but the two methods are independent in principle andin :type of apparatus employed.

Aside from economic factors, which are so variable -as to permit of'no positive state- `ments here, it .is well known thatall of these ymethods are open 'to criticism. llVith respect to v.the blast furnace method, it is recognized that .the use of a blast of hot air is not entirely satisfactory. Expensive apparatus is required to preheat and feed ,the air. 0f greater significance in the present connection is the fact that the use of a blast places :rectly utilized by la ldefinite lower limit on the size of the ore lumps which lmay be used. Pieces about one inch l'in diameter represent the generally accepted lower limit, -smaller pieces being Iunsuited for several reasons. Fine pieces of ore,

vor breeze, either fill the interstices between kthe larger lumps of the charge, and so restrict the passage of the hot gases, vor else they are swept away by the blast, being lost in the process and clogging the gas receiving apparatus. Another important factor is `that the use of hot air, containing approximatelyv '7 8 per vcent of inert nitrogem'serves as a dilutent of the Waste ases, reducing their heating value and limiting their application to other uses. It is also now commonly accepted that the nitrogen enters the molten metal to a limited extent, with deleterious results.

What has just been said of the blast furnace of course applies with equal force to the electrothermic method involving the use of a tower and hot blast. 'The direct gas reduc- .tion method, while not yet fully tested on a commercial scale, is obviously open to objection because of its admitted incompleteness, the necessity for gas feeding mechanism requiring delicate control at high temperatures, and the further disadvantage that the size of the ore particules must' be so large as to prevent their displacement by the hot blast. This last objection is apparent when considering the carbon pot furnace method, Where- .in thel large size of the particles is again necessary and there is an vineflicient utilization of heat and carbon.

The .present inventionv contemplates, in so far asl am aware, a different procedure than any of-those heretofore proposed, and lone free from the 'foregoing noted objections. The reduction reaction ofthe present linvention is not dependent upon the employment of a blast of hot air nor the circulation of reducing gases,-and so, at the outset. is to be distinguished from those methods noted which are. predicated upon these features. The method which I contemplate involves a more direct action between carbon and orc and under such conditions as to permit of the utilization of extremely finely divided I' particles of ore which are reduced to an agglomerated or semi-fluent state by use of the sensible heat developed in the action, `either 4from the arc or the sensible heat of the Waste gases, or both.' Thereafter the charge is injected directly into the arc itself to leffect a final reduction and melting of theresulting y sponge iron and gangue. In these features the present invention differs materially from the carbon reduction method previously described. The reduction is completely effected,

and the molten metal separated from the slag, in yone set of operations and in a unitari apparatus, and not in the separated an individual apparatus units such as previously has been suggested for utilizing both gaseous and direct carbon reduction.

lVit-hout intending to suggest that the principles of the invention are confined to the following outline vand Without pausing here to point out the numerous advantages and utilities of the method and attendant apparatus, it may be said in a generalvvay that I practice the invention advantageously in the following manner: Ore of suitable grade is mined in the usual manner and otherwise subjected to the usual preliminary treatments as in any other case of reduction. The crushed ore is then further crushed, advantageously being ground to a fine or pulverulent form so that all of it Will pass, for example, a `50 mesh sieve. The ore may be ground so as to pass a :250 mesh sieve but practical considerations such as economy of operation Will usually necessitate considerable tolerance above this size. It is desirable to crush the ore to a iineness which will permit `of a suiiicicnt amount of contact with carbon to insure proper reduction.

at the temperatures subsequently encountered are also added, andthe mixture then stirred until a homogeneous mass is obtained. The ideal conditi on would exist when each minute particle of ore was in direct contact with asimilar carbon particle, sothat the'direct reaction of reduction could be effected with a minimum expenditure of energy. While theoretical conditions are not possible in usual practice, this homogeneity of mixture may be obtained to a suiiicient degree by the manner just outlined.

The homogeneous charge is thenL introduced by a suitable mechanical feeding device into a cold end of a hollow 'and practically impervious tube, which, in the preferred form of the apparatus for practicing the method,

constitutes an electrode of an electric arc furnace. By means of the feeding device, the cha rge of ore is forced mechanically through thev electrode, which is horizontally disposed, passing from the cold end to the arc end, Where its temperature is raised to the temperature of the arc, say 6000 F. During the passage, the contacting particles of ore and carbon are increased in temperature and enter into a direct reducing action, ,iron or the oxide, FeO, being formed, and more or less carbon monoxide and carbon dioxidebeing liberated, This liberated gas, of course,en ters into other reducin actions with the ore, and also creates a decidged pressure within the tube or electrode. The pressure ofthe gas tends to force the reduced charge out of the electrode and directly into the arc, into which it is discharged or ejected as a frothy, semimolten. or spuming mass of ore in an advanced stage of reduction, spongy metallicv iron, and calcareous matter which forms a slag as soon as it passes the arc and has an opportunity to collect in a pool beneath.

There are certain precautions which must be taken, in view of the character of the rea`ctions Within the tube, in order to preserve one desirable advantage of the invention, namely, the utilization of finely ground ores. As previously noted, such ores are not suited for operations involving the use of a blast, as

they are blown awayfaster than they can be reduced. The liberation of gases Within the tube would have the same e1i`ect,.forcing the. powdered ore into the arc with explosive violence and insuicient treatment, if the tube were packed too tightly with charging material. Accordingly, enough void space should .be pro vided, and the rate of feeding be so adjusted, and the proportioning of the charging ingredients be so regulated, as to prevent this explosive and premature discharge of the ore. Another factor which is linsure a complete reduction.

useful in this connection, namely, the retentlon of the materials in the tube for a suiiicient length of time to insure a substantially com- Yplete reduction, `(e. g., conversion of 90 to 95 4percent of FesOil to Fe-l-FeO) is in making the charging opening'terminate directlyin the arc itself. The high temperature here encountered, andthe approaching temperatures in the tube at adjacent points, effects a rapid reduction of the ore to its frothycondition,

despite the increasing velocity imparted `to it by the formation of Waste gases. v

' After passing through the arc, and so being reduced almost completely, the ore and flux ing agents fall tol a' hearth which is maintained ata high temperature by the arc above. Here a complete reduction is insured, the metal' forming a liquid pool at the bottom of the furnace, and the slagloatin above. The molten metal and slagl may die tapped off from time to time,l andthen utilized or further/processed in known Ways.

Ithas been pointed out that thell present invention does'not contemplate the usefof an air blast, but on the contrary, the admission ofV atmospheric air is avoided asv muchas possible. However, the Waste gases must be accommodated, and, in the'preferred form of apparatus, I lead the Waste gases from the 'furnace through means serving to seal the -been utilized. As previously noted,'t`he reduced material falling tothe hearth of the furnace is not necessarily completely reduced, I contemplate, in one form of-apparatus, a vrevolving furnace, wherein, due Lto the revolution of the furnace, the molten mass of metal is constantly agitated and brought into contact with reducing gases in order to These gases come from the 'products of .reaction inthe tube, and are constantly drawn oil through a manifolding device to maintain a more or less constant composition of the' reducing atmosphere In passing out of the furnace, the

gases flow around the hollow electrode or charging tube, giving up, by conduction, some of their sensible heat which'is trans ferred through the tube Wall to institute the reducing reactions. Thereafter', the gases are Withdrawn under a suitable degree of suction which tends to draw the small amount of air ,'20

leaking around the joints ofthe furnace into the Waste gases, and so away from the molten metal. In this way the iron is protected from nitrogen.

The Withdrawal of the gases may be controlled so as to provide a' desired degree of pressure within the furnace,sucient to resist the explosive effects of the gases generated-within the tube, but insuflicient to force the waste gases back through the tube I and into the feeding mechanism of powdered waste gases, not so much to serve as a reducl ing agent, but as a promoter or accelerator of the direct reaction of reduction by carbon.

I -In order to obtain the contemplated use of reducing gas in this manner, it must be recalled that a large volume of gases is liberated in the tube, and that blasts through the tube should be avoided if finely divided ore 'is not to be displaced. Accordingly, in forming the charge, I merely saturate the voids between the particles with carbon' monoxide and carbon dioxide, so as to rovide a small quantity of reducing gas which serves to in- -stitute theI reduction within thek tube at a lower temperature than otherwise required. This saturation may be effected by stirring quietly the mixed materials in an atmosphere of gas, or permitting a trace of gas to flow in with the mixed materials as they are about to enter the tube. In another way, I add a little calcium carbonate or unburnt limestone to the charge, depending upon the breaking up ofthe carbonate at a' low temperature into limevand CO2 kto provide the promoting agent. As stated, the use of a promoter must be Adone with an appreciation of its purpose, which may otherwise be stated as a means to effect a more gradual development of the reaction to prevent the sudden formation of large volumes of gas having an explosive effect on the charge.

The a paratus may assume various forms,

l but the c arging tube should be horizontal, or

inclined to the horizon at an angle less vthan the angle of repose of the charge. The use4 of a revolving or oscillating furnace, to stir the molten charge, is advantageous, but a stationary `furnace may be employed. l rather long furnace may be used, with the Waste gases flowing around the charging tube, in order to utilize a greater amount of their sensible heat, and to effect other Veconomies in operation. Graphite electrodes have,

the longest life, but a charging' tube made of firebrick may be used and a carbon arc placed at its end. The charging tube should have a smooth bore, to prevent clogging, and

'a positive means should be employed to force the charge through the tube. Vertical tubes will notserve, as the charges would fall through them too rapidly to permit of any effective reduction.

A fuller understanding of the invention may be had by reference to the following description taken in connection with the drawings, wherein:

. Fig. l is a view, partially in cross-section and partially in side elevation, of a revolving furnace suit-able for reducing the ore ac cording tothe present process;

' asaaeee Fig. 2 `is la longitudinal cross-sectional view of a stationary type of furnace;

Fig. 3 is a transverse cross-sectional view of the apparatus shown in Fig. 2; and

Fig. 4 is a schematic view showing means to admix reducing gas with the charge.

l The apparatusshown in Fi 1 consists of a cylindrical shell'v 11 of metal aving a cylindrical side wall 12 and end walls 13 and 14 which are yaxially bored as indicated by theA The shell l1 is lined witha layer of fire brick 23 and a-wall 24 of magnesite, or other suitable heat resisting materlal. These pro-- tective layers are discontinuous around the axial openings in the end walls of the shell 11, to provide means for entering the interior of the furnace. Tap holes for the slag and molten metal are providedat suitable places in the lining and shell, in accordance with usual ractice.

Projecting into the furnace through the openings 15 and 16 are graphite electrodes 25 and 26, each being suitably supported and capable of lon 'tudinal adjustment, and also being provide with coolin means to maintain the outer ends of the e ectrodes at a low temperature. Each electrode is provided with a smooth hollow portion along its axis, as indicated by the numerals 27 and 28. The

A charge is fed into the furnace through these tubes. The electrodes mayv be made of any desired length andbe formed with male and female threaded ends, so that a fresh electrode may be attached to the outer end of an old electrode. There is shown `in the drawings but one electrode section, but it will be understood that more may be used. The extreme outer end of each electrode is provided with a threaded connection 29 for interengagement with a threaded end 31 of a feeding device to of courserather schematically illustrated,

and may `assume a variety of forms.

Surrounding each electrode at its point as y lll

of exit from the furnace is a cooling device which is also employed to remove waste gases from the furnace. The device consists of an annular metallic member 37 provided with an axial bore 38 for the reception of the electrode, and it is formed on" its outer end with a gland 39 that may be filled with packing material such as kieselguhr. The member 37 is mounted on a pedestal 4l which is longitudinally adjustable on a fixed base by means of a worm operated through a hand wheel 42. The member 37 may thus be moved with respect to the end walls of the furnace, and so form a very narrow gap through which air might seep into the furnace. This gap is further sealed by means of annular fianges 43 formed on the side walls 13 and 14 which surround the member 37. Packing rings of carbon may further be positioned between the members 37 and the fianges 43.

.The member 37 is formed with a closed internal chamber 44 for cooling liquid which is introduced and removed through pipes 45 and 46. Enclosed by the' several portions of the chamber 44 is an annular chamber 47 which is open at its inner portions for direct communication withthe openings in the furnace end walls. The chamber .47 is in communication with a gas holder, scrubber, or similar device by means lof a pipe line 48 leading through a suitable fan or like'means for withdrawing gases from the furnace. During the course of operation, the waste gases liberated in the furnace are drawn into the chamber 47 and so on out of the system, being disposed of in a variety of economical ways. The flow of gas through the openings 15 and 16 induces a slight flowy of air through the narrow gap ybetween the furnace wall and the member 37, and any air tending to leak into the furnace is accordingly diverted into the waste gas stream where it can do no harm. This slight suction action is desirable for the further reason that it prevents the escape of the flammable and poisonous waste gases into the air around the furnace. The cooling chamber 37 besides serving to prevent leakage of air into the furnace by virtue of .its adjustability, also cools the electrode so that the outer end is at room temperature. It will be noted that with this arrangement, the re actions in the tube are effected in the short l distance between the furnace wall and the arc.

In operation, the furnace is brought up to the required temperature and the powdered charge is fed into the arc through the tubes 27 and 28. In beginning the feeding, it may will not ensue. Thereafter, the regular fine charge is used. As the charge-comes into the zone of reaction at the furnace wall, the first stages of reduction occur, the gradgases maintained within the furnace.

The liberated gases are constantly beingl withdrawn by means of the suction apparatus, fiowing around the electrodes as they leave the furnace to supply part ofthe heat necessary to effect the initial reduction. These gases do not, however, come into directl contact with the charge in the tube. The suction applied is so chosen as to revent the gases from back-firing through t e tube, but a pressure within the furnace which will prevent explosive discharge from the tube is also maintained. The temperature or cur- -rent consumption may be regulated by longitudinal adjustment of the electrodes 25 and 26, or by changing the; voltage between them. The rate of feeding, and hence length of treatment in the tube, may lalso be adjusted.' by changing the speed of the 'screw conveyor 34; and, of course, it is obvious that lthe character of the charge itself may be varied over wide limits. This flexibility of adjustment and ease of control render the method and apparatus applicable to a'widel variety of ores and for use in the manufacture of a number of products.

After the requisite amount of charging stock has been fed into the furnace-the'molten bath is laved in the reducing atmosphere to insure complete reduction and such degree of purieation as may be desired. When the operation is complete the tap holes are knocked throughthe side wall of the furnace and the molten slag and metal run off separately to solidify. As soon as the reduced material is withdrawn the feeding may again be started, the furnace being rotated-and fresh quantities of charge being added. In some cases the rotation of the furnace need take place only after theyfeeding has ceased,

the subsequent lagitation or puddling being V done on the complete molten charge to obtain a final purification.

It will of course be understood that much I' axiliary apparatus other than that illustrated is employed in the operation ofv a commercial plant, but as such devices are lmown they need not be4 discussed in Idetail here. y f

the char e is fed in the manner previously describe The electrode 54 is-supported at a suitable number of oints along its length by means of w'alls 55 w ich are-so constructed as to deflect gases passing from the hearth 52 yto an'exit .pipe V56 posltioned at the end of the furnace remote from the hearth. Baffle walls 57, which are more or less angularly disposed to the axis of the furnace, are formed in the roof portion and, in association with the walls 55, providing means for causing the ases to move around the electrode 54 wit a spiral motion. v Due to the long length of the electrode 54, an appreciable amount of the sensible heat of the waste gases are utilized in effecting a high temperature reduction within/the electrode 54,' The material discharging from x the tube'yinto the furnace arc 52 is practicallyall reduced, and the molten iron and sIagma be tapped ofi' in a continuous man-l ner. I desired, an electrode` may be ver.

tically positioned throughthe roof of the furnace,l 51 to createal deflected arc acting upon the surface of the material on the furnace heartlnl .y l

, In Fig.' 4,' Ihave shown rather schematically one neai'ls for introducing a trace of reucingl gases into the incomin charge. Gases gare withdrawn from the urnace 60 through a pipe 6l andare sent to a gas holder by means of a pump 62 and pipes 63 and 64. Another pige 65 provided with a needle valve 66 lea s from the pipe 64 to the charging device'67. By vproper manipulation of the. valve 66 a limited amount of reducing f gas 'may be stirred into the charge as it enters the cold end ofthe electrodeiGS. The

charging hopper 69 is provided with a closed cover and the feeding 1s effected by means of one or more star wheels 70 positioned therein. From the foregoing description of certain embodiments of the process and apparatus for practicing the same, it will be apparent that. .I have provided a novel system for treating ores or crude metals to effect their,

purification and reduction. In view of the applicability? of the principles of the invention to a variety of materials and for a. numof special purposes, it will also be appreciated lthat the foregoing specifications are intended to be illustrative of the invention, and do notrepresent the limits thereof. It

willbe understood therefore that the sco e .u

of the invention should be determined by t e scope of the following claims.

' What is claimed is: g 1. The process of reducin iron ores which comprises homogeneously a mixing ore, carbon, and fluxing material, to form a char e, introducing said charge into a horizontally disposed closed tube, passing the charge through the tube and through a zone of the tube of gradually increasing temperature, maintaining the rate of passage through the 'comprises finely dividing and ho-mogeneous` y, which reducing reactions will be instituted,

tube and the temperature at such values as to effect a substantial reduction of the ore prior to discharge from the tube, and maintaining the external ressure at the discharge end of the tube ess than the pressure within the tube.

2. ln the electrothermic reductionl of liron ores, the process which com rises feeding a charge of ore, carbon, and uxing material into an electric arc'furnace through a hor-i zontally disposed hollow tube formed in a furnace electrode.v y

3. The process of reducing iron ores to metalliciron which com rises finely dividing and homogeneously a mixing iron ore, carbon, and a fluxing agent to form a charge, forcing said. charge through a substantia` ly horizontally disposed--hollow tube into ,an electric furnace, and withdrawing gases generated in the ensuing actions from the furnace at a low pressure preventingthe back, flow of said gases through the incoming charge. Y j' 4. The method of reducing iron ores which asf 9oly.. admixing iron ore, carbon and fluxing" material, enclosing the'mixture in a horizon tally disposed tube, moving the char through 4the tube and simultaneously su jecting the mixture to a gradually increasln 'and separately removing the molten iron and slag.

5. The process of reducing iro'n ores which comprises homogeneously admixing finely divided iron ore, carbon, and fluxing material, introducing the resulting charge into a horizontal-ly disposed closed tube, heating the charge in the tube to a .temperature at ibs moving the charge through the tube and simultaneously increasing the temperature, and discharging the contents ofthe tube into an electric arc while maintaining the pressure at the discharge -end of the tube less than the pressure within the tube. l

6. The process of reducing iron ores which comprises homogeneously' admixing finely divided iron ore, carbon', and fluxing material, further including in the mixture a limited supply of reducing gases, introducing the resulting charge into a horizontally disposed closed tube, heating the charge in the tube to a temperature at which reducing reactions will be instituted, moving the charge through the tube and simultaneously increasing the temperature, and discharging the contents of the tube into an electric arc whilemaintaining the pressure at the disa* 'i temperature, thereby effecting a substantie` y A .subjecting the'charge to an intense heat at the discharge end of the tube, subjecting the discharged material to vfurther heat to complete the reduction, separating the reduced iron from the slag formed vin the.

reaction, withdrawing gases generated in the reduction from the charge exteriorly of the tube, land separately removing the reduced metal and slag from the region of final heating.

8. The process of reducing iron ores which comprises finely dividing and homogeneously admixing iron ore, carbon, and fluxing material to form a. charge, enclosing the charge in a horizontally disposed hollow-tube, moving the mass through theytube and into regions of progressively increasing temperature to effect a substantial reduction of the ore, simultaneously maintaining the charge shielded from drafts of reducing gases formed by the complete reduction of the ore, discharging the partially reduced charge into an electric arc and into an atmosphere rich in carbon monoxide, heating the discharged mass in such atmosphere to effect a complete reduction of the ore to metal, and

continuously withdrawing a major portion of the gases formed in the reducing reactions from the region of the arc.

9. In the preparation of ferriferous metals from ores, the process which comprises homogeneously mixing finely divided ore and a reducing agent, providing an electric arc between horizontally disposed non-metallic electrodes formed with` longitudinally extending bores, heating the inner portion of said electrodes progressively from the ends remote from the arc to said arc, forcibly feeding the said mixture through said bores from the cold ends of the electrode and through the arc, and controlling the rate of movement of said mixture to effect the reduction there- 10. The method of reducing iron ores which comprises striking an electric arc between apair of horizontally disposed and hollow carbon electrodes, enclosing a portion i of said electrodes within a refractory housa homogeneously mixed and finely divided charge of ore, carbon a limited quantity of. reducing gas through said hollow electrodes from the exposed end to the arc ends thereof.

l1. In the electrothermic reduction of metallic ores, the process which comprises feeding a charge of ore, carbon, and fiuxing material into an electric arc furnace through a horizontally disposed hollowtube formed in a furnace electrode. Y

12. The process of reducing metallic ores to metal which comprises finely dividing and h'omogeneously admixing the ore, carbon and a iiuxing agent to form a charge, forcing said charge through a substantially horizontally` disposed hollow tube into an electric furnace,l and withdrawing gases generated nlthe ensuing action from the furnace-fat va, low pressure preventing the back flow of.v said gasesl through the incomin charge.

13. The process o reducing metallic ores n which comprises homogeneously admixing finely divided ore, carbon, and iiuxing material to form a charge, forcin the charge into a cold end of a horizontally di tube and out of a hot end thereof with gradual increase in temperature of the charge within the tube to enect a partial reduction of the ore, subjecting the charge to an intense heat at the discharge end of the tube, subjecting the discharged material to further heat to complete the reduction, separating the reduced metal from the slag formed in the reaction, withdrawing gases generated in and fluxing agent and sposed holy low tube, passing the material through the i the reduction from the charge exteriorly of the tube, and separately removing the reduced metal and slag from the region of final heating.

14. A method of propagating endothermic reactions in charges of solid material which comprises moving a charge of linely divided solid material throughV a conduit formed in an electrode of an electric arc, and controlling the rate of movement of said charg through said electrode.

l5. A method of propagating endothermicvv los reactions which comprises creating an elecv tric arc between substantially horizontall disposed electrodes, providing a vconduit through atleast one of said electrodes, in-

troducinga charge of solid material into said conduit at the end thereof remote from the" arc, forcibly feeding said finely divided charge through the electrode and into thev arc, introducing a quantity of gas into the remote end of the electrode, and maintaining i Y,

.a pressure on said gas to insure its movement through the electrode with said char e.

SYDNEY T. w rais.4 f

Geminiani?. or extinction Patent No. l,837,696. ramed December 22 ili, fo

SYDNEY T. WiiES,

It is hereby certified that the above numbereo paient was errnneously issued to "Wiles Electric Furnace Corporation", whereas said patent shnnhi mw been issued to Buffalo Electric Furnace Corporation. said corporation being assignee by mesne assignments ol the entire interest in said iin-mation, shown by the records of assignments in this office; and that the said Leiters Pasen: qmuid be read with this correction therein that the same may conform to the reu-ord of the case in the Patent Office.

Signed and sealed this 9th day of February, A. D. ,w32

M, J. Moore,

(Seal) Acting Commissioner of Patents. 

